US10868308B2 - Cathode slurry for lithium ion battery - Google Patents

Cathode slurry for lithium ion battery Download PDF

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US10868308B2
US10868308B2 US16/313,875 US201716313875A US10868308B2 US 10868308 B2 US10868308 B2 US 10868308B2 US 201716313875 A US201716313875 A US 201716313875A US 10868308 B2 US10868308 B2 US 10868308B2
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cathode
active material
cathode active
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Kam Piu HO
Ranshi WANG
Peihua SHEN
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GRST International Ltd
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    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/621—Binders
    • H01M4/622—Binders being polymers
    • H01M4/623—Binders being polymers fluorinated polymers
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/131—Electrodes based on mixed oxides or hydroxides, or on mixtures of oxides or hydroxides, e.g. LiCoOx
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00—Secondary cells; Manufacture thereof
    • H01M10/05—Accumulators with non-aqueous electrolyte
    • H01M10/052—Li-accumulators
    • H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/04—Processes of manufacture in general
    • H01M4/0402—Methods of deposition of the material
    • H01M4/0404—Methods of deposition of the material by coating on electrode collectors
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/04—Processes of manufacture in general
    • H01M4/0471—Processes of manufacture in general involving thermal treatment, e.g. firing, sintering, backing particulate active material, thermal decomposition, pyrolysis
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/136—Electrodes based on inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/139—Processes of manufacture
    • H01M4/1391—Processes of manufacture of electrodes based on mixed oxides or hydroxides, or on mixtures of oxides or hydroxides, e.g. LiCoOx
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/139—Processes of manufacture
    • H01M4/1397—Processes of manufacture of electrodes based on inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/621—Binders
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/621—Binders
    • H01M4/622—Binders being polymers
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/624—Electric conductive fillers
    • H01M4/625—Carbon or graphite
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/64—Carriers or collectors
    • H01M4/66—Selection of materials
    • H01M4/663—Selection of materials containing carbon or carbonaceous materials as conductive part, e.g. graphite, carbon fibres
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M2004/021—Physical characteristics, e.g. porosity, surface area
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/139—Processes of manufacture
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10—Energy storage using batteries

Definitions

  • This invention relates to electrode slurries.
  • this invention relates to a cathode slurry for the use in lithium-ion batteries.
  • LIBs Lithium-ion batteries
  • EV electric vehicles
  • grid energy storage Due to rapid market development of electric vehicles (EV) and grid energy storage, high-performance, low-cost LIBs are currently offering one of the most promising options for large-scale energy storage devices.
  • a lithium ion battery includes a separator, a cathode and an anode.
  • electrodes are prepared by dispersing fine powders of an active battery electrode material, a conductive agent, and a binder material in an appropriate solvent. The dispersion can be coated onto a current collector such as a copper or aluminum metal foil, and then dried at elevated temperature to remove the solvent. Sheets of the cathode and anode are subsequently stacked or rolled with the separator separating the cathode and anode to form a battery.
  • the critical process steps in battery production are coating and drying operations of cathode. Therefore, preparation of the cathode slurries is an essential first step towards the production of good quality batteries.
  • Residual solvent in the coating layer due to incomplete drying can contribute to adherence problems which will eventually affect the performance and quality of the batteries.
  • One way to remove residual solvent from an electrode is to dry the electrode for a long period of time under high temperature. However, prolonged heating at high temperature may cause the coating to disintegrate due to aging of polymeric binder. The change of electrode characteristics is detrimental to the proper functioning of the completed battery.
  • CN Patent Application No. 105149186 A describes a method for drying the electrode coating.
  • the coated electrode is inductively heated by an induction heating coil to heat the metallic current collector to a desired temperature.
  • the coated electrode may be non-uniformly heated due to nonuniform distribution of induced current density in the coil. This can create a problem with respect to obtaining rapid heating to a uniform temperature, affecting the quality of the coating.
  • U.S. Patent Application No. 20160087262 A1 describes a cathode active material with an average particle size of 2 to 8 ⁇ m for a high energy density lithium-ion battery.
  • the cathode active material comprises a lithium nickel manganese composite oxide having a small and uniform particle size to improve the output characteristics of a lithium-ion battery. A specific discharge capacity of 150-200 mAh/g was obtained.
  • 10 wt. % of binding agent is needed for binding the cathode active material and conductive material to the cathode current collector because of high specific surface area of the cathode active material.
  • a large amount of binding agent in the electrode coating will reduce the energy density of a lithium-ion battery.
  • the resulting cathode is required to be dried in a vacuum dryer at high temperature for 12 hours. The long time required for drying is considered to be not suitable for large scale production.
  • U.S. Pat. No. 8,900,753 B2 describes a cathode material which includes a mixture of a cathode active material having a large primary particle size and another cathode active material having a small primary particle size to ensure high safety and output characteristics.
  • the coated cathode is also required to be dried at a temperature of 120° C. This will cause high energy consumption and high production cost on large-scale production of batteries.
  • a lithium-ion battery cathode slurry comprising: a cathode active material, a conductive agent, a binder material, and a solvent, wherein the cathode active material has a particle size D50 in the range from about 10 ⁇ m to about 50 ⁇ m, and wherein the slurry coated onto a current collector having a wet film thickness of about 100 ⁇ m has a drying time of about 5 minutes or less under an environment having a temperature of about 60° C. to about 90° C. and a relative humidity of about 25% to about 40%.
  • the cathode active material is selected from the group consisting of LiCoO 2 , LiNiO 2 , LiNi x Mn y O 2 , Li 1+z Ni x Mn y Co 1 ⁇ x ⁇ y O 2 , LiNi x Co y Al z O 2 , LiV 2 O 5 , LiTiS 2 , LiMoS 2 , LiMnO 2 , LiCrO 2 , LiMn 2 O 4 , LiFeO 2 , LiFePO 4 , LiNi 0.5 Mn 1.5 O 4 , LiNi 0.4 Mn 1.6 O 4 , composites thereof, and combinations thereof, wherein each x is independently from 0.3 to 0.8; each y is independently from 0 to 0.45; and each z is independently from 0 to 0.2.
  • the cathode active material is present in an amount from 30% to 65% by weight; the conductive agent is present in an amount from 0.8% to 5% by weight; the binder material is present in an amount from 0.5% to 6% by weight; and the solvent is present in an amount from 30% to 60% by weight, wherein the combined weight % value of all components does not exceed 100 wt. %; and wherein all weight % values are based on the total weight of the slurry.
  • the cathode active material is present in an amount from 35% to 50% by weight; the conductive agent is present in an amount from 1% to 4% by weight; the binder material is present in an amount from 0.8% to 3.5% by weight; and the solvent is present in an amount from 40% to 55% by weight, wherein the combined weight % value of all components does not exceed 100 wt. %; and wherein all weight % values are based on the total weight of the slurry.
  • the cathode active material has a D10 value of at least 3 ⁇ m. In certain embodiments, the cathode active material has a D90 value of less than or equal to 80 ⁇ m. In some embodiments, the ratio D90/D10 of the cathode active material is from about 3 to about 10, or from about 5 to about 8.
  • the particle size distribution of the cathode active material is bimodal with a first peak at about 12 ⁇ m and a second peak at about 30 ⁇ m.
  • the conductive agent is selected from the group consisting of carbon, carbon black, graphite, expanded graphite, graphene, graphene nanoplatelets, carbon fibres, carbon nano-fibers, graphitized carbon flake, carbon tubes, carbon nanotubes, activated carbon, mesoporous carbon, and combinations thereof.
  • the binder material is selected from the group consisting of styrene-butadiene rubber, acrylated styrene-butadiene rubber, acrylonitrile copolymer, acrylonitrile-butadiene rubber, nitrile butadiene rubber, acrylonitrile-styrene-butadiene copolymer, acryl rubber, butyl rubber, fluorine rubber, polytetrafluoroethylene, polyethylene, polypropylene, ethylene/propylene copolymers, polybutadiene, polyethylene oxide, chlorosulfonated polyethylene, polyvinylpyrrolidone, polyvinylpyridine, polyvinyl alcohol, polyvinyl acetate, polyepichlorohydrin, polyphosphazene, polyacrylonitrile, polystyrene, latex, acrylic resins, phenolic resins, epoxy resins, carboxymethyl cellulose, hydroxypropyl cellulose, cellulose
  • the solvent is selected from the group consisting of N-methyl-2-pyrrolidone, dimethylformamide, dimethyl sulfoxide, acetonitrile, butylene carbonate, propylene carbonate, ethyl bromide, tetrahydrofuran, dimethyl carbonate, diethyl carbonate, ethyl methyl carbonate, methyl propyl carbonate, ethylene carbonate, water, pure water, de-ionized water, distilled water, ethanol, isopropanol, methanol, acetone, n-propanol, t-butanol, and combinations thereof.
  • the solvent has a boiling point of less than 200° C., less than 180° C., less than 160° C., less than 140° C., less than 120° C., or less than 100° C.
  • the viscosity of the slurry is in the range from about 1,000 mPa ⁇ s to about 4,500 mPa ⁇ s.
  • the vapor pressure of the solvent is at least 15 kPa.
  • the pH of the slurry is from about 7 to about 11.
  • the coated slurry film is dried by a box oven, a conveyor oven, or a hot plate.
  • the slurry coated onto the current collector in the form of a film has a drying time of about 5 minutes or less.
  • a positive electrode for a lithium-ion battery comprising: a cathode current collector and a cathode electrode layer dispersed on the cathode current collector, wherein the cathode electrode layer is formed using the cathode slurry prepared by the method disclosed herein.
  • a lithium-ion battery comprising: a cathode, an anode and a separator interposed between the cathode and the anode, wherein at least one of the cathode is the positive electrode prepared by the method disclosed herein.
  • conductive agent refers to a chemical or a substance that increases the electrical conductivity of an electrode.
  • binder material refers to a chemical or a substance that can be used to hold the active battery electrode material and conductive agent in place.
  • applied or “applying” refers to an act of laying or spreading a layer of slurry on a surface of the current collector.
  • current collector refers to a support for coating the active battery electrode material and a chemically inactive high electron conductor for keeping an electric current flowing to electrodes during discharging or charging a secondary battery.
  • the term “still air” refers to the air surrounding the coating being substantially motionless. In the absence of air flow, a wind speed of less than 0.2 m/s was observed at a position 1 cm above the top surface of the coating surface. In some embodiments, the wind speed is less than 0.1 m/s. In certain embodiments, the wind speed is 0 m/s.
  • major component of a composition refers to the component that is more than 50%, more than 55%, more than 60%, more than 65%, more than 70%, more than 75%, more than 80%, more than 85%, more than 90%, or more than 95% by weight or volume, based on the total weight or volume of the composition.
  • minor component of a composition refers to the component that is less than 50%, less than 45%, less than 40%, less than 35%, less than 30%, less than 25%, less than 20%, less than 15%, less than 10%, or less than 5% by weight or volume, based on the total weight or volume of the composition.
  • homogenizer refers to an equipment that can be used for homogenization of materials.
  • homogenization refers to a process of reducing a substance or material to small particles and distributing it uniformly throughout a fluid. Any conventional homogenizers can be used for the method disclosed herein. Some non-limiting examples of the homogenizer include stirring mixers, blenders, mills (e.g., colloid mills and sand mills), ultrasonicators, atomizers, rotor-stator homogenizers, and high pressure homogenizers.
  • C rate refers to the charging or discharging rate of a cell or battery, expressed in terms of its total storage capacity in Ah or mAh. For example, a rate of 1 C means utilization of all of the stored energy in one hour; a 0.1 C means utilization of 10% of the energy in one hour and the full energy in 10 hours; and a 5 C means utilization of the full energy in 12 minutes.
  • ampere-hour (Ah) refers to a unit used in specifying the storage capacity of a battery.
  • a battery with 1 Ah capacity can supply a current of one ampere for one hour or 0.5 A for two hours, etc. Therefore, 1 Ampere-hour (Ah) is the equivalent of 3600 coulombs of electrical charge.
  • miniampere-hour (mAh) also refers to a unit of the storage capacity of a battery and is 1/1,000 of an ampere-hour.
  • battery cycle life refers to the number of complete charge/discharge cycles a battery can perform before its nominal capacity falls below 80% of its initial rated capacity.
  • doctor blading refers to a process for fabrication of large area films on rigid or flexible substrates.
  • a coating thickness can be controlled by an adjustable gap width between a coating blade and a coating surface, which allows the deposition of variable wet layer thicknesses.
  • transfer coating or “roll coating” refers to a process for fabrication of large area films on rigid or flexible substrates.
  • a slurry is applied on the substrate by transferring a coating from the surface of a coating roller with pressure.
  • a coating thickness can be controlled by an adjustable gap width between a metering blade and a surface of the coating roller, which allows the deposition of variable wet layer thicknesses.
  • the thickness of the coating is controlled by adjusting the gap between a metering roller and a coating roller.
  • particle size D50 refers to a volume-based accumulative 50% size (D50) which is a particle size at a point of 50% on an accumulative curve (i.e., a diameter of a particle in the 50th percentile (median) of the volumes of particles) when the accumulative curve is drawn so that a particle size distribution is obtained on the volume basis and the whole volume is 100%.
  • the particle size D50 means a volume-averaged particle size of secondary particles which are formed by mutual agglomeration and sintering of primary particles, and in a case where the particles are composed of the primary particles only, it means a volume-averaged particle size of the primary particles.
  • D10 means a volume-based accumulative 10% size (i.e., a diameter of a particle in the 10th percentile of the volumes of particles)
  • D90 means a volume-based accumulative 90% size (i.e., a diameter of a particle in the 90th percentile of the volumes of particles).
  • vapor pressure of a fluid refers to the pressure exerted by the vapor of that fluid with the liquid phase in thermodynamic equilibrium at a given temperature in a closed system.
  • solid content refers to the amount of non-volatile material remaining after evaporation.
  • R R L +k*(R U ⁇ R L ), wherein k is a variable ranging from 1 percent to 100 percent with a 1 percent increment, i.e., k is 1 percent, 2 percent, 3 percent, 4 percent, 5 percent, . . . , 50 percent, 51 percent, 52 percent, . . . , 95 percent, 96 percent, 97 percent, 98 percent, 99 percent, or 100 percent.
  • any numerical range defined by two R numbers as defined in the above is also specifically disclosed.
  • a lithium-ion battery cathode slurry comprising: a cathode active material, a conductive agent, a binder material, and a solvent, wherein the cathode active material has a particle size D50 in the range from about 10 ⁇ m to about 50 ⁇ m, and wherein the slurry coated onto a current collector having a wet film thickness of about 100 ⁇ m has a drying time of about 5 minutes or less under an environment having a temperature of about 60° C. to about 90° C. and a relative humidity of about 25% to about 40%.
  • cathode active material having a smaller particle size is preferred.
  • the average particle size of the cathode active material is preferred being in the range of 0.05 ⁇ m to 5 ⁇ m.
  • An electrode in which cathode active materials of different particle diameters are included has also been used as a cathode for a lithium secondary battery. Accordingly, the spaces between the large diameter particles are filled with the small diameter particles.
  • a dense coating will retard evaporation of solvent from the interior of the coating.
  • the curing steps of current processes are time consuming. The drying time can be shortened upon exposure to high temperatures. However, this often leads to poor electrode quality and significantly poorer cell performance because of nonuniform drying.
  • a slurry comprising a cathode active material having particles with a particular range of particle size and size ratio that allows a relatively high drying rate has not been developed, and a slurry capable of high processability is desired. Therefore, there is always a need for a new cathode slurry that is simple, reliable and cost-effective to be used for making a lithium ion battery with high quality and consistent performance.
  • the cathode active material is selected from the group consisting of LiCoO 2 (LCO), LiNiO 2 (LNO), LiNi x Mn y O 2 , Li 1+z Ni x Mn y Co 1 ⁇ x ⁇ y O 2 , LiNi x Co y Al z O 2 , LiV 2 O 5 , LiTiS 2 , LiMoS 2 , LiMnO 2 , LiCrO 2 , LiMn 2 O 4 (LMO), LiFeO 2 , LiFePO 4 (LFP), LiNi 0.5 Mn 1.5 O 4 , LiNi 0.4 Mn 1.6 O 4 , and combinations thereof, wherein each x is independently from 0.3 to 0.8; each y is independently from 0.1 to 0.45; and each z is independently from 0 to 0.2.
  • the cathode active material is selected from the group consisting of LiCoO 2 , LiNiO 2 , LiNi x Mn y O 2 , Li 1+z Ni x Mn y Co 1 ⁇ x ⁇ y O 2 , LiNi x Co y Al z O 2 , LiV 2 O 5 , LiTiS 2 , LiMoS 2 , LiMnO 2 , LiCrO 2 , LiMn 2 O 4 , LiFeO 2 , LiFePO 4 , LiNi 0.5 Mn 1.5 O 4 , LiNi 0.4 Mn 1.6 O 4 , and combinations thereof, wherein each x is independently from 0.4 to 0.6; each y is independently from 0.2 to 0.4; and each z is independently from 0 to 0.1.
  • the cathode active material is not LiCoO 2 , LiNiO 2 , LiV 2 O 5 , LiTiS 2 , LiMoS 2 , LiMnO 2 , LiCrO 2 , LiMn 2 O 4 , LiFeO 2 , LiFePO 4 , LiNi 0.5 Mn 1.5 O 4 , or LiNi 0.4 Mn 1.6 O 4 .
  • the cathode active material is LiNi 0.33 Mn 0.33 Co 0.33 O 2 (NMC333), LiNi 0.5 Mn 0.3 Co 0.2 O 2 (NMC532), LiNi 0.4 Mn 0.4 Co 0.2 O 2 , LiNi 0.6 Mn 0.2 Co 0.2 O 2 (NMC622), LiNi 0.8 Mn 0.1 Co 0.1 O 2 (NMC811) or LiNi 0.8 Co 0.15 Al 0.05 O 2 (NCA).
  • NMC333 LiNi 0.33 Mn 0.33 Co 0.33 O 2
  • NMC532 LiNi 0.5 Mn 0.3 Co 0.2 O 2
  • NMC622 LiNi 0.4 Mn 0.4 Co 0.2 O 2
  • NMC622 LiNi 0.6 Mn 0.2 Co 0.2 O 2
  • NMC811 LiNi 0.8 Mn 0.1 Co 0.1 O 2
  • NCA LiNi 0.8 Co 0.15 Al 0.05 O 2
  • the cathode active material is doped with a dopant selected from the group consisting of Fe, Ni, Mn, Al, Mg, Zn, Ti, La, Ce, Sn, Zr, Ru, Si, Ge, and combinations thereof.
  • the dopant is not Fe, Ni, Mn, Mg, Zn, Ti, La, Ce, Ru, Si, or Ge.
  • the dopant is not Al, Sn, or Zr.
  • the cathode active material is not doped with a dopant.
  • the cathode active material comprises or is a core-shell composite comprising a core comprising a lithium transition metal oxide and a shell formed by coating the surface of the core with a transition metal oxide.
  • the lithium transition metal oxide is selected from the group consisting of LiCoO 2 , LiNiO 2 , LiNi x Mn y O 2 , Li 1+z Ni x Mn y Co 1 ⁇ x ⁇ y O 2 , LiNi x Co y Al z O 2 , LiV 2 O 5 , LiTiS 2 , LiMoS 2 , LiMnO 2 , LiCrO 2 , LiMn 2 O 4 , LiFeO 2 , LiFePO 4 , LiNi 0.5 Mn 1.5 O 4 , LiNi 0.4 Mn 1.6 O 4 , and combinations thereof, wherein each x is independently from 0.3 to 0.8; each y is independently from 0.1 to 0.45; and each z is independently from 0 to
  • the transition metal oxide is selected from the group consisting of Fe 2 O 3 , MnO 2 , Al 2 O 3 , MgO, ZnO, TiO 2 , La 2 O 3 , CeO 2 , SnO 2 , ZrO 2 , RuO 2 , and combinations thereof.
  • the cathode active material comprises or is a core-shell composite having a core and shell structure, wherein the core and the shell each independently comprise a lithium transition metal oxide selected from the group consisting of LiCoO 2 , LiNiO 2 , LiNi x Mn y O 2 , Li 1+z Ni x Mn y Co 1 ⁇ x ⁇ y O 2 , LiNi x Co y Al z O 2 , LiV 2 O 5 , LiTiS 2 , LiMoS 2 , LiMnO 2 , LiCrO 2 , LiMn 2 O 4 , LiFeO 2 , LiFePO 4 , LiNi 0.5 Mn 1.5 O 4 , LiNi 0.4 Mn 1.6 O 4 , and combinations thereof, wherein each x is independently from 0.3 to 0.8; each y is independently from 0.1 to 0.45; and each z is independently from 0 to 0.2.
  • a lithium transition metal oxide selected from the group consisting of LiCoO 2
  • the core and the shell each independently comprise two or more lithium transition metal oxides.
  • the two or more lithium transition metal oxides in the core and the shell may be the same, or may be different or partially different.
  • the two or more lithium transition metal oxides are uniformly distributed over the core. In certain embodiments, the two or more lithium transition metal oxides are not uniformly distributed over the core.
  • each of the lithium transition metal oxides in the core and the shell is independently doped with a dopant selected from the group consisting of Fe, Ni, Mn, Al, Mg, Zn, Ti, La, Ce, Sn, Zr, Ru, Si, Ge, and combinations thereof.
  • the core and the shell each independently comprise two or more doped lithium transition metal oxides.
  • the two or more doped lithium transition metal oxides are uniformly distributed over the core. In certain embodiments, the two or more doped lithium transition metal oxides are not uniformly distributed over the core.
  • the diameter of the core is from about 5 ⁇ m to about 45 ⁇ m, from about 5 ⁇ m to about 35 ⁇ m, from about 5 ⁇ m to about 25 ⁇ m, from about 10 ⁇ m to about 40 ⁇ m, or from about 10 ⁇ m to about 35 ⁇ m.
  • the thickness of the shell is from about 15 ⁇ m to about 45 ⁇ m, from about 15 ⁇ m to about 30 ⁇ m, from about 15 ⁇ m to about 25 ⁇ m, from about 20 ⁇ m to about 30 ⁇ m, or from about 20 ⁇ m to about 35 ⁇ m.
  • the diameter or thickness ratio of the core and the shell are in the range of 15:85 to 85:15, 25:75 to 75:25, 30:70 to 70:30, or 40:60 to 60:40.
  • the volume or weight ratio of the core and the shell is 80:20, 70:30, 60:40, 50:50, 40:60, or 30:70.
  • the cathode active material does not comprise a core-shell structure. In some embodiments, the cathode active material is not doped with a dopant Fe, Ni, Mn, Al, Mg, Zn, Ti, La, Ce, Sn, Zr, Ru, Si, or Ge.
  • the core and the shell each independently does not comprise LiCoO 2 , LiNiO 2 , LiNi x Mn y O 2 , Li 1+z Ni x Mn y Co 1 ⁇ x ⁇ y O 2 , LiNi x Co y Al z O 2 , LiV 2 O 5 , LiTiS 2 , LiMoS 2 , LiMnO 2 , LiCrO 2 , LiMn 2 O 4 , LiFeO 2 , LiFePO 4 , LiNi 0.5 Mn 1.5 O 4 , or LiNi 0.4 Mn 1.6 O 4 , wherein each x is independently from 0.3 to 0.8; each y is independently from 0.1 to 0.45; and each z is independently from 0 to 0.2.
  • the cathode active material of the present invention has a particle size D50 in the range from about 10 ⁇ m to about 50 ⁇ m, from about 10 ⁇ m to about 45 ⁇ m, from about 10 ⁇ m to about 40 ⁇ m, from about 10 ⁇ m to about 35 ⁇ m, from about 10 ⁇ m to about 30 ⁇ m, from about 10 ⁇ m to about 25 ⁇ m, from about 15 ⁇ m to about 45 ⁇ m, from about 15 ⁇ m to about 30 ⁇ m, from about 20 ⁇ m to about 50 ⁇ m, from about 20 ⁇ m to about 40 ⁇ m, from about 20 ⁇ m to about 30 ⁇ m, from about 25 ⁇ m to about 45 ⁇ m, from about 25 ⁇ m to about 40 ⁇ m, from about
  • the particle diameter D50 of the cathode active material is less than 50 ⁇ m, less than 45 ⁇ m, less than 40 ⁇ m, less than 35 ⁇ m, less than 30 ⁇ m, less than 25 ⁇ m, less than 20 ⁇ m, or less than 15 ⁇ m. In some embodiment, the particle diameter D50 of the cathode active material is greater than 10 ⁇ m, greater than 15 ⁇ m, greater than 20 ⁇ m, greater than 25 ⁇ m, greater than 30 ⁇ m, greater than 35 ⁇ m, greater than 40 ⁇ m, or greater than 45 ⁇ m.
  • the particle diameter D50 of the cathode active material is about 10 ⁇ m, about 11 ⁇ m, about 12 ⁇ m, about 13 ⁇ m, about 14 ⁇ m, about 15 ⁇ m, about 16 ⁇ m, about 17 ⁇ m, about 18 ⁇ m, about 19 ⁇ m, about 20 ⁇ m, about 21 ⁇ m, about 22 ⁇ m, about 23 ⁇ m, about 24 ⁇ m, about 25 ⁇ m, about 26 ⁇ m, about 27 ⁇ m, about 28 ⁇ m, about 29 ⁇ m, about 30 ⁇ m, about 31 ⁇ m, about 32 ⁇ m, about 33 ⁇ m, about 34 ⁇ m, about 35 ⁇ m, about 36 ⁇ m, about 37 ⁇ m, about 38 ⁇ m, about 39 ⁇ m, about 40 ⁇ m, about 41 ⁇ m, about 42 ⁇ m, about 43 ⁇ m, about 44 ⁇ m, about 45 ⁇ m, about 46 ⁇ m, about 47 ⁇ m, about 48 ⁇ m, about 49
  • the cathode active material has a particle size D10 from about 3 ⁇ m to about 20 ⁇ m, from about 3 ⁇ m to about 10 ⁇ m, from about 3 ⁇ m to about 8 ⁇ m, from about 1 ⁇ m to about 10 ⁇ m, from about 1 ⁇ m to about 8 ⁇ m, from about 1 ⁇ m to about 5 ⁇ m, from about 2 ⁇ m to about 10 ⁇ m, from about 2 ⁇ m to about 5 ⁇ m, or from about 2 ⁇ m to about 8 ⁇ m.
  • the cathode active material has a particle size D90 from about 20 ⁇ m to about 80 ⁇ m, from about 30 ⁇ m to about 80 ⁇ m, from about 40 ⁇ m to about 80 ⁇ m, from about 50 ⁇ m to about 80 ⁇ m, from about 30 ⁇ m to about 70 ⁇ m, from about 30 ⁇ m to about 60 ⁇ m, from about 20 ⁇ m to about 50 ⁇ m, from about 20 ⁇ m to about 60 ⁇ m, or from about 40 ⁇ m to about 60 ⁇ m.
  • the ratio D90/D10 of the cathode active material is from about 3 to about 15, from about 3 to about 10, from about 3 to about 8, from about 5 to about 15, from about 5 to about 10, from about 5 to about 8, from about 7.5 to about 20, from about 10 to about 20, or from about 10 to about 15.
  • the amount of the cathode active material is at least 10%, at least 15%, at least 20%, at least 25%, at least 27.5%, at least 30%, at least 32.5%, at least 35%, at least 37.5%, at least 40%, at least 42.5%, at least 45%, at least 47.5%, at least 50%, at least 52.5%, at least 55%, at least 57.5, or at least 60% by weight or volume, based on the total weight or volume of the slurry.
  • the amount of the cathode active material is at most 25%, at most 27.5%, at most 30%, at most 32.5%, at most 35%, at most 37.5%, at most 40%, at most 42.5%, at most 45%, at most 47.5%, at most 50%, at most 52.5%, at most 55%, at most 57.5%, or at most 60% by weight or volume, based on the total weight or volume of the slurry.
  • the amount of the cathode active material is about 40%, about 41%, about 42%, about 43%, about 44%, about 45%, about 46%, about 47%, about 48%, about 49%, about 50%, about 51%, about 52%, about 53%, about 54%, or about 55% by weight or volume, based on the total weight or volume of the slurry.
  • the conductive agent in the slurry is for enhancing the electrical conductivity of a cathode.
  • the conductive agent is selected from the group consisting of carbon, carbon black, graphite, expanded graphite, graphene, graphene nanoplatelets, carbon fibres, carbon nano-fibers, graphitized carbon flake, carbon tubes, carbon nanotubes, activated carbon, mesoporous carbon, and combinations thereof.
  • the conductive agent is not carbon, carbon black, graphite, expanded graphite, graphene, graphene nanoplatelets, carbon fibres, carbon nano-fibers, graphitized carbon flake, carbon tubes, carbon nanotubes, activated carbon, or mesoporous carbon.
  • the particle size of conductive agent is from about 10 nm to about 100 nm, from about 10 nm to about 50 nm, from about 10 nm to about 45 nm, from about 10 nm to about 40 nm, from about 10 nm to about 35 nm, from about 10 nm to about 30 nm, from about 10 nm to about 25 nm, from about 10 nm to about 20 nm, from about 10 nm to about 15 nm, from about 20 nm to about 50 nm, from about 20 nm to about 40 nm, from about 25 nm to about 50 nm, from about 30 nm to about 50 nm, or from about 30 nm to about 40 nm.
  • the binder material is selected from the group consisting of styrene-butadiene rubber, acrylated styrene-butadiene rubber, acrylonitrile copolymer, acrylonitrile-butadiene rubber, nitrile butadiene rubber, acrylonitrile-styrene-butadiene copolymer, acryl rubber, butyl rubber, fluorine rubber, polytetrafluoroethylene, polyethylene, polypropylene, ethylene/propylene copolymers, polybutadiene, polyethylene oxide, chlorosulfonated polyethylene, polyvinylpyrrolidone, polyvinylpyridine, polyvinyl alcohol, polyvinyl acetate, polyepichlorohydrin, polyphosphazene, polyacrylonitrile, polystyrene, latex, acrylic resins, phenolic resins, epoxy resins, carboxymethyl cellulose, hydroxypropyl cellulose, cellulose
  • the binder material is selected from the group consisting of styrene-butadiene rubber, carboxymethyl cellulose, polyvinylidene fluoride, acrylonitrile copolymer, polyacrylic acid, polyacrylonitrile, poly(vinylidene fluoride)-hexafluoropropene, latex, a salt of alginic acid, and combinations thereof.
  • the binder material is selected from SBR, CMC, PAA, a salt of alginic acid, or a combination thereof.
  • the binder material is acrylonitrile copolymer.
  • the binder material is polyacrylonitrile.
  • the binder material is free of styrene-butadiene rubber, carboxymethyl cellulose, polyvinylidene fluoride, acrylonitrile copolymer, polyacrylic acid, polyacrylonitrile, poly(vinylidene fluoride)-hexafluoropropene, latex, or a salt of alginic acid.
  • the amount of each of the conductive agent and binder material is independently at least 0.1%, at least 0.25%, at least 0.5%, at least 0.75%, at least 1%, at least 1.25%, at least 1.5%, at least 1.75%, at least 2%, at least 2.25%, at least 2.5%, at least 2.75%, at least 3%, at least 4%, at least 5%, at least 10%, at least 15%, at least 20%, at least 25%, at least 30%, at least 35%, at least 40%, at least 45%, or at least 50% by weight or volume, based on the total weight or volume of the slurry.
  • the amount of each of the conductive agent and binder material is independently at most 0.1%, at most 0.25%, at most 0.5%, at most 0.75%, at most 1%, at most 1.25%, at most 1.5%, at most 1.75%, at most 2%, at most 2.25%, at most 2.5%, at most 2.75%, at most 3%, at most 4%, at most 5%, at most 10%, at most 15%, at most 20%, at most 25%, at most 30%, at most 35%, at most 40%, at most 45%, or at most 50% by weight or volume, based on the total weight or volume of the slurry.
  • the amount of the conductive agent is from about 0.02% to about 1%, from about 0.02% to about 0.5%, from about 0.02% to about 0.25%, from about 0.05% to about 1%, from about 0.05% to about 0.5%, from about 0.12% to about 1.25%, from about 0.12% to about 1%, from about 0.25% to about 2.5%, from about 0.5% to about 2.5%, from about 0.5% to about 2%, from about 1% to about 3%, from about 1% to about 2.5%, from about 1% to about 2%, from about 1% to about 1.5%, from about 1.5% to about 3%, from about 1% to about 2.5%, from about 1.5% to about 3.5%, or from about 2.5% to about 5% by weight or volume, based on the total weight or volume of the slurry.
  • the amount of the conductive agent is about 0.5%, about 0.75%, about 1%, about 1.25%, about 1.5%, about 1.75%, about 2%, about 2.25%, about 2.5%, about 2.75%, or about 3% by weight or volume, based on the total weight or volume of the slurry.
  • the amount of the binder material is about 0.5%, about 0.75%, about 1%, about 1.25%, about 1.5%, about 1.75%, about 2%, about 2.25%, about 2.5%, about 2.75%, about 3%, about 3.5%, about 4%, about 4.5%, or about 5% by weight or volume, based on the total weight or volume of the slurry.
  • the slurry is prepared by mixing the cathode active material with auxiliary materials such as conductive agent and binder material in a solvent.
  • the mixing process aims to achieve a uniform dispersion of the particles of the cathode active material, conductive agent and binder material in a solvent.
  • ketone solvents include methyl propyl ketone, methyl isobutyl ketone, ethyl propyl ketone, diisobutyl ketone, acetophenone, N-methyl-2-pyrrolidone (NMP), acetone, and the like.
  • acetate solvents include ethyl acetate, butyl acetate, isobutyl acetate, and the like.
  • propionate esters such as n-butyl propionate, n-pentyl propionate and ethylene glycol monoethylether propionate are also suitable.
  • the volatile solvent or minor component is methyl ethyl ketone, ethanol, ethyl acetate or a combination thereof.
  • the solvent is a mixture of water and one or more water-miscible minor components.
  • the solvent is a mixture of water and a minor component selected from methanol, ethanol, isopropanol, n-propanol, t-butanol, n-butanol, and combinations thereof.
  • the volume ratio of water and the minor component is from about 51:49 to about 100:1.
  • the solvent is water. Since the composition of the slurry does not contain any organic solvent, expensive, restrictive and complicated handling of organic solvents is avoided during manufacture of slurries.
  • Some non-limiting examples of water include tap water, bottled water, purified water, pure water, distilled water, de-ionized water, D 2 O, or a combination thereof.
  • the solvent is de-ionized water.
  • the solvent comprises a volatile solvent, a nonvolatile solvent or a combination thereof.
  • the solvent comprises a mixture of NMP and at least one alcohol solvent selected from the group consisting of n-butanol, isopropanol, n-propanol, ethanol, and methanol.
  • the solvent comprises a mixture of NMP and ethanol or a mixture of NMP and isopropanol.
  • the solvent comprises a mixture of NMP and dimethyl carbonate. In other embodiments, the solvent comprises a mixture of NMP and water, water and ethanol, or water and dimethyl carbonate. In certain embodiments, the volatile solvent is the major component which provides slurry with rapid drying properties. In some embodiments, the volume ratio of volatile solvent and the nonvolatile solvent is from about 51:49 to about 100:1.
  • a slurry having a solvent with high vapor pressure can be dried at a higher rate.
  • the vapor pressure of the solvent at a temperature from about 65° C. to 90° C. is independently from about 0.01 kPa to about 200 kPa, from about 0.01 kPa to about 150 kPa, from about 0.01 kPa to about 100 kPa, from about 0.1 kPa to about 200 kPa, from about 0.1 kPa to about 150 kPa, from about 0.1 kPa to about 100 kPa, from about 0.3 kPa to about 200 kPa, from about 0.3 kPa to about 150 kPa, from about 0.3 kPa to about 100 kPa, from about 0.3 kPa to about 80 kPa, from about 0.3 kPa to about 60 kPa, from about 0.3 kPa to about 40 kPa, from about 0.3 kPa to about 20
  • the vapor pressure of the solvent at a temperature from about 60° C. to 90° C. is independently less than 200 kPa, less than 150 kPa, less than 100 kPa, less than 90 kPa, less than 80 kPa, less than 70 kPa, less than 60 kPa, less than 50 kPa, less than 40 kPa, less than 30 kPa, less than 20 kPa, less than 10 kPa, less than 5 kPa, less than 1 kPa, less than 0.5 kPa, less than 0.3 kPa, or less than 0.1 kPa. In some embodiments, the vapor pressure of the solvent at a temperature from about 60° C.
  • to 90° C. is independently at least 0.01 kPa, at least 0.05 kPa, at least 0.1 kPa, at least 0.5 kPa, at least 1 kPa, at least 5 kPa, at least 10 kPa, at least 20 kPa, at least 30 kPa, at least 40 kPa, at least 50 kPa, at least 60 kPa, at least 70 kPa, at least 80 kPa, at least 90 kPa, at least 100 kPa, at least 150 kPa, or at least 200 kPa.
  • a slurry having a solvent with a low boiling point can be dried at a faster rate.
  • the boiling point of the solvent is from about 40° C. to about 250° C., from about 40° C. to about 200° C., from about 40° C. to about 150° C., from about 40° C. to about 100° C., from about 40° C. to about 90° C., from about 40° C. to about 80° C., from about 40° C. to about 70° C., from about 40° C. to about 60° C., from about 60° C. to about 100° C., from about 60° C. to about 90° C., from about 60° C. to about 80° C., or from about 60° C. to about 70° C.
  • the boiling point of the solvent is less than 250° C., less than 200° C., less than 150° C., less than 100° C., less than 90° C., less than 80° C., less than 70° C., less than 60° C., or less than 50° C. In some embodiments, the boiling point of the solvent is at least 40° C., at least 50° C., at least 60° C., at least 70° C., at least 80° C., at least 90° C., at least 100° C., at least 150° C., or at least 200° C.
  • the solvent is present in an amount from about 20% to about 80%, from about 20% to about 70%, from about 20% to about 60%, from about 20% to about 50%, from about 20% to about 40%, from about 30% to 50%, from about 30% to about 40%, from about 40% to about 70%, from about 40% to about 60%, from about 40% to about 50%, from about 50% to about 80%, from about 50% to about 70%, from about 50% to about 60%, from about 25% to about 60%, from about 25% to about 50%, from about 25% to about 45%, from about 45% to about 60%, from about 45% to about 55%, or from about 45% to about 50% by weight or volume, based on the total weight or volume of the slurry.
  • the solvent is present in an amount less than 80%, less than 70%, less than 60%, less than 55%, less than 50%, less than 45%, less than 40%, less than 35%, less than 30%, less than 25%, or less than 20% by weight or volume, based on the total weight or volume of the slurry. In some embodiments, the solvent is present in an amount at least 15%, at least 20%, at least 25%, at least 30%, at least 35%, at least 40%, at least 45%, at least 50%, at least 55%, at least 60%, at least 70%, or at least 80% by weight or volume, based on the total weight or volume of the slurry.
  • the amount of solvent is about 40%, about 41%, about 42%, about 43%, about 44%, about 45%, about 46%, about 47%, about 48%, about 49%, about 50%, about 51%, about 52%, about 53%, about 54%, about 55%, about 56%, about 57%, about 58%, about 59%, or about 60% by weight or volume, based on the total weight or volume of the slurry.
  • the weight percentage of solvent is more than total weight percentage of cathode active material, conductive agent and binder material. In certain embodiments, the weight percentage of solvent is less than total weight percentage of cathode active material, conductive agent and binder material. In some embodiments, the weight percentage of solvent is equal to the total weight percentage of cathode active material, conductive agent and binder material.
  • the weight percentage of cathode active material is more than the weight percentage of conductive agent.
  • the ratio of the weight percentage of cathode active material to the weight percentage of conductive agent in the slurry is from about 1 to about 100, from about 1 to about 80, from about 1 to about 60, from about 1 to about 50, from about 10 to about 50, from about 10 to about 40, from about 10 to about 35, from about 10 to about 30, from about 10 to about 25, from about 10 to about 20, from about 20 to about 60, from about 20 to about 50, from about 20 to about 45, from about 20 to about 40, from about 30 to about 50, from about 30 to about 40, from about 40 to about 60, from about 40 to about 50, from about 20 to about 30, or from about 20 to about 25.
  • the ratio of the weight percentage of cathode active material to the weight percentage of conductive agent in the slurry is less than 100, less than 80, less than 60, less than 50, less than 45, less than 40, less than 35, less than 30, less than 25, less than 20, or less than 10. In certain embodiments, the ratio of the weight percentage of cathode active material to the weight percentage of conductive agent in the slurry is at least 1, at least 10, at least 20, at least 25, at least 30, at least 35, at least 40, at least 45, at least 50, at least 55, at least 60, or at least 80.
  • the ratio of the weight percentage of cathode active material to the weight percentage of conductive agent in the slurry is about 15, about 16, about 17, about 18, about 19, about 20, about 21, about 22, about 23, about 24, about 25, about 26, about 27, about 28, about 29, or about 30.
  • the weight percentage of cathode active material is more than the weight percentage of binder material.
  • the ratio of the weight percentage of cathode active material to the weight percentage of binder material in the slurry is from about 1 to about 100, from about 1 to about 80, from about 1 to about 60, from about 1 to about 50, from about 5 to about 50, from about 5 to about 45, from about 5 to about 40, from about 5 to about 35, from about 5 to about 30, from about 5 to about 25, from about 5 to about 20, from about 5 to about 15, from about 15 to about 50, from about 15 to about 40, from about 15 to about 35, from about 15 to about 30, from about 15 to about 25, or from about 15 to about 20.
  • the ratio of the weight percentage of cathode active material to the weight percentage of binder material in the slurry is less than 100, less than 80, less than 60, less than 50, less than 45, less than 40, less than 35, less than 30, less than 25, less than 20, less than 15, or less than 10. In some embodiments, the ratio of the weight percentage of cathode active material to the weight percentage of binder material in the slurry is at least 5, at least 10, at least 15, at least 20, at least 25, at least 30, at least 35, at least 40, at least 45, at least 50, at least 60, at least 70, or at least 80.
  • the ratio of the weight percentage of cathode active material to the weight percentage of binder material in the slurry is about 15, about 16, about 17, about 18, about 19, about 20, about 21, about 22, about 23, about 24, about 25, about 26, about 27, about 28, about 29, about 30, about 31, about 32, about 33, about 34, about 35, about 36, about 37, about 38, about 39, or about 40.
  • the weight percentage of binder material is more than the weight percentage of conductive agent. In certain embodiments, the weight percentage of binder material is less than the weight percentage of conductive agent. In some embodiments, the weight percentage of binder material is equal to the weight percentage of conductive agent.
  • the ratio of the weight percentage of binder material to the weight percentage of conductive agent is from about 0.1 to about 5, from about 0.5 to about 4.5, from about 0.5 to about 4, from about 0.5 to about 3.5, from about 0.5 to about 3, from about 0.5 to about 2.5, from about 0.5 to about 2, from about 0.5 to about 1.5, from about 0.5 to about 1, from about 1 to about 5, from about 1 to about 4, from about 1 to about 3, from about 1 to about 2, or from about 1 to about 1.5. In some embodiments, the ratio of the weight percentage of binder material to the weight percentage of conductive agent is less than 5, less than 4.5, less than 4, less than 3.5, less than 3, less than 2.5, less than 2, less than 1.5, less than 1, or less than 0.5. In certain embodiments, the ratio of the weight percentage of binder material to the weight percentage of conductive agent is at least 0.5, at least 1, at least 1.5, at least 2, at least 2.5, at least 3, at least 3.5, at least 4, or at least 4.5.
  • Electrode coating layers are typically prepared by coating a suspension of particles containing a cathode active material, conductive agent and binder material onto a support and allowing the suspension to dry into a thin film. It is generally desired that the cathode slurry can dry as quickly as possible. This improves productivity of a coating system, thus reducing overall processing time.
  • the cathode slurry comprises a cathode active material as a main component.
  • One method of preparing a rapid-dry slurry is to use cathode active material having large particle size. Particle size distribution plays a crucial role in determining specific surface area of the cathode active material. The larger surface area allows a greater interaction with the solvent, which results in slower drying.
  • the cathode active material comprises a mixture of particles of two size distributions where a particle size of a peak of a second distribution being greater than a particle size of a peak of a first distribution.
  • a first peak of the bimodal distribution may be between about 5 ⁇ m and about 20 ⁇ m
  • a second peak of the bimodal distribution may be between about 20 ⁇ m and about 40 ⁇ m.
  • the particle size distribution of the cathode active material is bimodal with a first peak at about 10 ⁇ m and a second peak at about 25 ⁇ m. The packing density increases when the small particles fill the interstices between the larger particles.
  • the difference between the diameters at the two peaks of the distribution is less than or equal to 80%, less than or equal to 60%, less than or equal to 50%, or less than or equal to 35%.
  • the weight ratio of the cathode active material having a particle size of a peak of a second distribution to the cathode active material having a particle size of a peak of a first distribution is from 3:1 to 5:1. In certain embodiments, the weight ratio of the cathode active material having a particle size of a peak of a second distribution to the cathode active material having a particle size of a peak of a first distribution is 5:1, 4:1 or 3:1.
  • the dispersing agent is a nonionic surfactant, an anionic surfactant, a cationic surfactant, an amphoteric surfactant, or a combination thereof.
  • suitable nonionic surfactant include an alkoxylated alcohol, a carboxylic ester, a polyethylene glycol ester, and combinations thereof.
  • suitable alkoxylated alcohol include ethoxylated and propoxylated alcohols.
  • the nonionic surfactant is nonylphenol ethoxylate.
  • anionic surfactant examples include a salt of an alkyl sulfate, an alkyl polyethoxylate ether sulfate, an alkyl benzene sulfonate, an alkyl ether sulfate, a sulfonate, a sulfosuccinate, a sarcosinate, and combinations thereof.
  • the anionic surfactant comprises a cation selected from the group consisting of sodium, potassium, ammonium, and combinations thereof.
  • the anionic surfactant is lithium dodecyl sulfate, sodium dodecylbenzene sulfonate, or sodium stearate.
  • suitable cationic surfactant include an ammonium salt, a phosphonium salt, an imidazolium salt, a sulfonium salt, and combinations thereof.
  • suitable ammonium salt include stearyl trimethylammonium bromide (STAB), cetyl trimethylammonium bromide (CTAB), myristyl trimethylammonium bromide (MTAB), trimethylhexadecyl ammonium chloride and combinations thereof.
  • amphoteric surfactant are surfactants that contain both cationic and anionic groups.
  • the cationic group is ammonium, phosphonium, imidazolium, sulfonium, or a combination thereof.
  • the anionic hydrophilic group is carboxylate, sulfonate, sulfate, phosphonate, or a combination thereof.
  • the dispersing agent is selected from the group consisting of lithium dodecyl sulfate, trimethylhexadecyl ammonium chloride, alcohol ethoxylate, nonylphenol ethoxylate, sodium dodecylbenzene sulfonate, sodium stearate, and combinations thereof.
  • the formulation of the slurry of the present invention prevents agglomeration of particles in water without the use of surfactant and allows rapid drying of the slurry when coated on a current collector.
  • the slurry is free of surfactant.
  • the slurry is free of a nonionic surfactant, an anionic surfactant, a cationic surfactant, or an amphoteric surfactant.
  • the slurry can be homogenized by a homogenizer.
  • the homogenizing step reduces or eliminates the potential aggregation of the cathode active material and the conductive agent and enhances dispersion of each ingredient in the slurry. Any equipment that can homogenize the slurry can be used.
  • the homogenizer is a stirring mixer, a blender, a mill, an ultrasonicator, a rotor-stator homogenizer, or a high pressure homogenizer.
  • the homogenizer is an ultrasonicator. Any ultrasonicator that can apply ultrasound energy to agitate and disperse particles in a sample can be used herein.
  • the ultrasonicator is a probe-type ultrasonicator or an ultrasonic flow cell.
  • the viscosity of the slurry affects the quality of the ultimate coating. If the viscosity of the slurry is too high, it may result in the formation of a non-uniform coating. Further, if the viscosity of the slurry is too low, a satisfactory film is hardly obtainable.
  • Particle agglomeration increases the drying time of the slurry because solvent may be trapped within the agglomerates, thereby making evaporation of solvent more difficult.
  • Using larger cathode material particles reduces the occurrence of particle agglomeration.
  • the pH of the slurry also affects the stability of particles in the slurry. When the pH of the slurry is out of the desired range, binder material is more difficult to be dispersed uniformly in the slurry. This may cause uneven drying and shrinkage of the coated film.
  • the pH of the slurry may be affected by dispersing a nickel-rich cathode active material in an aqueous solvent because nickel-rich material may react with water to cause an increase in pH. Large-sized particles of the cathode active material has a small specific surface area Therefore, pH variation due to reaction of cathode active material with water is reduced.
  • the pH of the cathode slurry is from about 7 to about 11, from about 7 to about 10.5, from about 7 to about 10, from about 7 to about 9.5, from about 7 to about 9, from about 7 to about 8.5, from about 7 to about 8, from about 7 to about 7.5, from about 7.5 to about 11, from about 7.5 to about 10, from about 7.5 to about 9, from about 7.5 to about 8, from about 8 to about 11, from about 8 to about 10.5, from about 8 to about 10, from about 8 to about 9.5, from about 8 to about 9, from about 8 to about 8.5, from about 9 to about 11, or from about 9 to about 10.
  • the pH of the cathode slurry is less than 12, less than 11.5, less than 11, less than 10.5, less than 10, less than 9.5, less than 9, less than 8.5, less than 8, less than 7.5, or less than 7. In some embodiments, the pH of the cathode slurry is at least 7, at least 7.5, at least 8, at least 8.5, at least 9, at least 9.5, at least 10, at least 10.5, or at least 11. In certain embodiments, the pH of the cathode slurry is about 7, about 7.5, about 8, about 8.5, about 9, about 9.5, about 10, about 10.5, or about 11.
  • the cathode slurry has a viscosity from about 500 mPa ⁇ s to about 6,000 mPa ⁇ s, from about 500 mPa ⁇ s to about 5,500 mPa ⁇ s, from about 500 mPa ⁇ s to about 5,000 mPa ⁇ s, from about 500 mPa ⁇ s to about 4,500 mPa ⁇ s, from about 500 mPa ⁇ s to about 4,000 mPa ⁇ s, from about 500 mPa ⁇ s to about 3,500 mPa ⁇ s, from about 500 mPa ⁇ s to about 3,000 mPa ⁇ s, from about 1,000 mPa ⁇ s to about 6,000 mPa ⁇ s, from about 1,000 mPa ⁇ s to about 5,500 mPa ⁇ s, from about 1,000 mPa ⁇ s to about 5,000 mPa ⁇ s, from about 1,000 mPa ⁇ s to about 4,500 mPa ⁇ s, from about 1,000 mPa ⁇ s to about 4,000 mP
  • the cathode slurry has a viscosity less than 6,000 mPa ⁇ s, less than 5,500 mPa ⁇ s, less than 5,000 mPa ⁇ s, less than 4,500 mPa ⁇ s, less than 4,000 mPa ⁇ s, less than 3,500 mPa ⁇ s, less than 3,000 mPa ⁇ s, less than 2,500 mPa ⁇ s, less than 2,000 mPa ⁇ s, or less than 1,000 mPa ⁇ s.
  • the cathode slurry has viscosity more than 1,000 mPa ⁇ s, more than 1,500 mPa ⁇ s, more than 2,000 mPa ⁇ s, more than 2,500 mPa ⁇ s, more than 3,000 mPa ⁇ s, more than 3,500 mPa ⁇ s, more than 4,000 mPa ⁇ s, more than 4,500 mPa ⁇ s, more than 5,000 mPa ⁇ s, or more than 5,500 mPa ⁇ s.
  • the solid content of the cathode slurry is from about 20% to about 80%, from about 20% to about 70%, from about 20% to about 60%, from about 20% to about 50%, from about 20% to about 40%, from about 30% to about 70%, from about 30% to about 60%, from about 30% to about 50%, from about 30% to about 40%, from about 40% to about 70%, from about 40% to about 60%, from about 40% to about 50%, from about 25% to about 60%, from about 35% to about 60%, or from about 45% to about 60% by weight, based on the total weight of the cathode slurry.
  • the solid content of the cathode slurry is less than 80%, less than 70%, less than 60%, less than 55%, less than 50%, less than 45%, less than 40%, less than 35%, less than 30%, or less than 25% by weight, based on the total weight of the cathode slurry. In some embodiments, the solid content of the cathode slurry is at least 20%, at least 25%, at least 30%, at least 35%, at least 40%, at least 45%, at least 50%, at least 55%, or at least 60% by weight, based on the total weight of the cathode slurry.
  • the solid content of the cathode slurry is about 40%, about 41%, about 42%, about 43%, about 44%, about 45%, about 46%, about 47%, about 48%, about 49%, about 50%, about 51%, about 52%, about 53%, about 54%, about 55%, about 56%, about 57%, about 58%, about 59%, or about 60% by weight, based on the total weight of the cathode slurry.
  • the homogenized slurry can be applied on a current collector to form a coated film on the current collector.
  • the current collector acts to collect electrons generated by electrochemical reactions of the active battery electrode material or to supply electrons required for the electrochemical reactions.
  • each of the current collectors of the positive and negative electrodes which can be in the form of a foil, sheet or film, is independently stainless steel, titanium, nickel, aluminum, copper or electrically-conductive resin.
  • the current collector of the positive electrode is an aluminum thin film.
  • the current collector of the negative electrode is a copper thin film.
  • the surface of current collector is not pre-treated.
  • the current collector has a thickness from about 6 ⁇ m to about 100 ⁇ m since thickness will affect the volume occupied by the current collector within a battery and the amount of the active battery electrode material and hence the capacity in the battery.
  • the coating process is performed using a doctor blade coater, a slot-die coater, a transfer coater, a spray coater, a roll coater, a dip coater, or a curtain coater.
  • the thickness of the coated film on the current collector is from about 10 ⁇ m to about 300 ⁇ m, or from about 20 ⁇ m to about 100 ⁇ m.
  • the coated film on the current collector can be dried by a dryer to obtain the battery electrode.
  • Any dryer that can dry the coated film on the current collector can be used herein.
  • the dryer are a batch drying oven, a box-type drying oven, a hot plate, a conveyor drying oven, and a microwave drying oven.
  • the conveyor drying oven include a conveyor hot air drying oven, a conveyor resistance drying oven, a conveyor inductive drying oven, and a conveyor microwave drying oven.
  • the conveyor drying oven for drying the coated film on the current collector includes one or more heating sections, wherein each of the heating sections is individually temperature controlled, and wherein each of the heating sections may include independently controlled heating zones.
  • the conveyor drying oven comprises a first heating section positioned on one side of the conveyor and a second heating section positioned on an opposing side of the conveyor from the first heating section, wherein each of the first and second heating sections independently comprises one or more heating elements and a temperature control system connected to the heating elements of the first heating section and the second heating section in a manner to monitor and selectively control the temperature of each heating section.
  • the cathode slurry comprises at least one solvent having a boiling point below 150° C.
  • the choice and amount of solvent affects the curing conditions. Selection of solvent with a lower boiling point enables faster drying at lower temperature. A lower temperature can avoid crack or embrittlement of a cathode electrode layer.
  • the coated film on the current collector can be dried at a temperature from about 45° C. to about 100° C., from about 50° C. to about 100° C., from about 55° C. to about 100° C., from about 50° C. to about 90° C., from about 50° C. to about 80° C., from about 55° C. to about 80° C., from about 55° C.
  • the coated film on the current collector can be dried at a temperature less than 100° C., less than 95° C., less than 90° C., less than 85° C., less than 80° C., less than 75° C., less than 70° C., less than 65° C., less than 60° C., less than 55° C., less than 50° C., less than 45° C., or less than 40° C.
  • the coated film on the current collector can be dried at a temperature higher than 40° C., higher than 45° C., higher than 50° C., higher than 55° C., higher than 60° C., higher than 65° C., higher than 70° C., higher than 75° C., higher than 80° C., higher than 85° C., or higher than 90° C.
  • the coated film should not be dried under windy conditions which may cause non-uniform slurry distribution and in turn affect the quality of the coated electrode.
  • the coated film on the current collector can be dried under still air conditions.
  • the coated film on the current collector can be dried under an environment having a wind speed between 0.2 m/s and 1 m/s, or between 0.2 m/s and 0.7 m/s.
  • the wind speed is less than 0.7 m/s, less than 0.5 m/s, less than 0.4 m/s, less than 0.3 m/s, less than 0.2 m/s, or less than 0.1 m/s.
  • the wind speed is 0 m/s.
  • the coated film on the current collector can be dried under an environment having a relative humidity from about 0% to about 60%, from about 10% to about 50%, from about 20% to about 50%, from about 20% to about 40%, from about 25% to about 40%, from about 15% to about 50%, from about 15% to about 40%, from about 15% to about 30%, from about 15% to about 25%, or from about 20% to about 30%.
  • the relative humidity is less than 50%, less than 45%, less than 40%, less than 35%, less than 30%, less than 25%, less than 20%, less than 15%, or less than 10%.
  • the cathode slurry disclosed herein can be dried in a short period of time.
  • the coated film can be dried for a time period from about 1 minute to about 15 minutes, from about 1 minute to about 10 minutes, from about 1 minute to about 8 minutes, from about 1 minute to about 5 minutes, from about 1 minute to about 4 minutes, from about 1 minute to about 3 minutes, from about 1 minute to about 2 minutes, from about 1.5 minutes to about 5 minutes, from about 1.5 minutes to about 4 minutes, from about 1.5 minutes to about 3 minutes, from about 2 minutes to about 10 minutes, from about 2 minutes to about 5 minutes, from about 2 minutes to about 4 minutes, from about 2 minutes to about 3 minutes, from about 3 minutes to about 5 minutes, from about 3 minutes to about 4 minutes, from about 4 minutes to about 5 minutes, from about 2.5 minutes to about 5 minutes, from about 2.5 minutes to about 4 minutes, or from about 3.5 minutes to about 5 minutes.
  • the coated film can be dried for a time period of less than 12 hours, less than 8 hours, less than 4 hours, less than 2 hours, less than 1 hour, less than 45 minutes, less than 30 minutes, less than 15 minutes, less than 13 minutes, less than 10 minutes, less than 9 minutes, less than 8 minutes, less than 7 minutes, less than 6 minutes, less than 5 minutes, less than 4.5 minutes, less than 4 minutes, less than 3.5 minutes, less than 3 minutes, less than 2.5 minutes, less than 2 minutes, or less than 1.5 minutes. If the drying rate is too slow, manufacturing efficiency suffers.
  • solvent has been removed from the coated film. Comparison of the mass of the coated electrode dried for a predetermined time to a coated electrode dried for a prolonged period of time is used as a measurement of the extent of drying. During the prolonged period of drying, the amount of solvent that can be removed from the coated electrode dried for a predetermined time is less than 2 percent by weight, based on total weight of the coated electrode involving drying for a predetermined time period.
  • the battery electrode is formed.
  • the battery electrode is compressed mechanically in order to enhance the density of the electrode.
  • a lithium-ion battery comprising a cathode, an anode and a separator interposed between the cathode and the anode, wherein at least one of the cathode is the positive electrode prepared by the method disclosed herein.
  • the wind speed was determined by measuring the wind speed at a position 1 cm above the top surface of the coated film by means of a commercially available anemometer.
  • the particle size was analyzed using a MicroBrook 2000LD particle size analyzer (obtained from Brookhaven Instruments Cooperation, US).
  • the slurry viscosity was determined with a NDJ-5S viscometer (obtained from Shanghai Hengping Scientific Instrument Co., China).
  • a particulate cathode active material Li 1.02 Ni 0.35 Mn 0.34 Co 0.31 O 2 (NMC333) was obtained by a co-precipitation method followed by calcination at 850° C.
  • the calcinated product was crushed by a jet mill (LNJ-6A, obtained from Mianyang Liuneng Powder Equipment Co., Ltd., Sichuan, China) for about 1 hour, followed by passing through a 270-mesh sieve to obtain a cathode active material having a particle size D50 of about 42 ⁇ m.
  • a positive electrode slurry was prepared by mixing 92 wt. % cathode active material prepared by method described above, 4 wt. % carbon black (SuperP; obtained from Timcal Ltd, Bodio, Switzerland) as a conductive agent, 4 wt. % polyvinylidene fluoride (PVDF; Solef® 5130, obtained from Solvay S. A., Belgium) as a binder material, which were dispersed in a mixed solvent containing 50 wt. % N-methyl-2-pyrrolidone (NMP; purity of ⁇ 99%, Sigma-Aldrich, USA) and 50 wt.
  • NMP N-methyl-2-pyrrolidone
  • % acetone purity of ⁇ 99%, Sigma-Aldrich, USA
  • the slurry was homogenized by a planetary stirring mixer.
  • the viscosity of the positive electrode slurry was 1,850 mPa ⁇ s.
  • the homogenized slurry was coated onto one side of an aluminum foil having a thickness of 20 ⁇ m as a current collector using a doctor blade coater (MSK-AFA-III, obtained from Shenzhen Kejing Star Technology Ltd., China) with a gap width of 100 ⁇ m.
  • the coated film on the aluminum foil was dried in a box-type resistance oven (DZF-6020, obtained from Shenzhen Kejing Star Technology Co. Ltd., China) at 65° C. under still air condition having a wind speed between 0.1 m/s and 0.2 m/s.
  • the relative humidity inside the oven was 25-35%.
  • the drying time was about 3 minutes.
  • a negative electrode slurry was prepared by mixing 90 wt. % of hard carbon (HC; purity of 99.5%, obtained from Ruifute Technology Ltd., Shenzhen, Guangdong, China) with 1.5 wt. % carboxymethyl cellulose (CMC, BSH-12, DKS Co. Ltd., Japan) and 3.5 wt. % SBR (AL-2001, NIPPON A&L INC., Japan) as a binder material, and 5 wt. % carbon black as a conductive agent, which were dispersed in deionized water to form another slurry with a solid content of 50 wt. %.
  • hard carbon HC
  • CMC carboxymethyl cellulose
  • SBR A&L INC., Japan
  • the slurry was coated onto both sides of a copper foil having a thickness of 9 ⁇ m using a doctor blade coater (MSK-AFA-III, Shenzhen Kejing Star Technology Ltd., China) with a gap width of 120 ⁇ m.
  • the coated film on the copper foil was dried by an electrically heated conveyor oven at 80° C. for 10 minutes to obtain a negative electrode.
  • a pouch cell was assembled by packaging the dried electrode assembly in a case made of an aluminum-plastic laminated film.
  • the cathode and anode electrode plates were kept apart by separators and the case was pre-formed.
  • An electrolyte was then filled into the case holding the packed electrodes in high-purity argon atmosphere with moisture and oxygen content ⁇ 1 ppm.
  • the electrolyte was a solution of LiPF 6 (1 M) in a mixture of ethylene carbonate (EC), ethyl methyl carbonate (EMC) and dimethyl carbonate (DMC) in a volume ratio of 1:1:1.
  • EC ethylene carbonate
  • EMC ethyl methyl carbonate
  • DMC dimethyl carbonate
  • the cyclability performance of the pouch cell was tested by charging and discharging at a constant current rate of 1C between 3.0 V and 4.2 V.
  • the electrochemical tests show good electrochemical stability of the battery in a wide range of potential, as well as outstanding cycle performance.
  • the formulation of the cathode slurry of Example 1 is shown in Table 1 below.
  • the drying conditions of the coated cathode film of Example 1 are shown in Table 2 below.
  • the electrochemical performance of the pouch cell of Example 1 are shown in Table 3 below.
  • a particulate cathode active material Li 0.98 Mn 2.1 O 4 (LMO) was obtained by a co-precipitation method followed by calcination at 900° C.
  • the calcinated product was crushed by a jet mill for about 1 hour, followed by passing through a 400-mesh sieve to obtain a cathode active material having a particle size D50 of about 15 ⁇ m.
  • a positive electrode slurry was prepared by mixing 92 wt. % cathode active material prepared by method described above, 3 wt. % carbon black (SuperP; obtained from Timcal Ltd, Bodio, Switzerland) as a conductive agent, and 1 wt. % CMC (BSH-12, DKS Co. Ltd., Japan), 2 wt. % SBR (AL-2001, NIPPON A&L INC., Japan) and 2 wt. % polyvinylidene fluoride (PVDF; Solef® 5130, obtained from Solvay S. A., Belgium) as a binder material, which were dispersed in a mixed solvent containing 50 wt. % deionized water and 50 wt. % ethanol to form a slurry with a solid content of 50 wt. %.
  • the slurry was homogenized by a planetary stirring mixer.
  • a viscosity of the positive electrode slurry was 1,650 mP
  • the homogenized slurry was coated onto one side of an aluminum foil having a thickness of 20 ⁇ m as a current collector using a doctor blade coater with a gap width of 100 ⁇ m.
  • the coated film on the aluminum foil was dried by an electrically heated conveyor oven (TH-1A, obtained from Nanjing Tonghao Drying Equipment Co. Ltd., China) at 60° C. at a conveyor speed of about 5 meters/minute.
  • the oven was arranged in a substantially windless environment. A wind speed between 0.3 m/s and 0.5 m/s inside the oven was detected.
  • the relative humidity inside the oven was 25-40%.
  • the drying time was about 4.5 minutes.
  • a particulate cathode active material Li 1.05 Mn 1.94 O 4 (LMO) was obtained by a co-precipitation method followed by calcination at 900° C.
  • the calcinated product was crushed by a ball milling for about 1.5 hours, followed by passing through a 325-mesh sieve to obtain the cathode active material having a particle size D50 of about 28 ⁇ m.
  • a positive electrode slurry was prepared by mixing 94 wt. % cathode active material prepared by method described above, 3 wt. % carbon black (SuperP; obtained from Timcal Ltd, Bodio, Switzerland) as a conductive agent, and 1.5 wt. % polyacrylic acid (PAA, #181285, obtained from Sigma-Aldrich, US) and 1.5 wt. % polyacrylonitrile (LA 132, Chengdu Indigo Power Sources Co., Ltd., China) as a binder material, which were dispersed in deionized water to form a slurry with a solid content of 50 wt. %.
  • the slurry was homogenized by a planetary stirring mixer.
  • the viscosity of the positive electrode slurry was 2,300 mPa ⁇ s.
  • the homogenized slurry was coated onto one side of an aluminum foil having a thickness of 20 ⁇ m as a current collector using a doctor blade coater with a gap width of 100 ⁇ m.
  • the coated film on the aluminum foil was dried by an electrically heated conveyor oven at 75° C. at a conveyor speed of about 8 meters/minute.
  • the oven was arranged in a substantially windless environment. A wind speed between 0.1 m/s and 0.3 m/s inside the oven was detected.
  • the relative humidity inside the oven was 25-40%.
  • the drying time was about 3 minutes.
  • CR2032 coin-type Li cells were assembled in an argon-filled glove box.
  • the coated cathode and anode sheets prepared by the method described in Example 1 were cut into disc-form positive and negative electrodes for coin cell assembly.
  • the electrolyte was a solution of LiPF 6 (1 M) in a mixture of ethylene carbonate (EC), ethyl methyl carbonate (EMC) and dimethyl carbonate (DMC) in a volume ratio of 1:1:1.
  • the coin cells were analyzed in a constant current mode using a multi-channel battery tester (BTS-4008-5V10mA, obtained from Neware Electronics Co. Ltd, China). After 1 cycle at C/20 was completed, they were charged and discharged at a rate of C/2. The charging/discharging cycling tests of the cells were performed between 3.0 and 4.2 V with at a current density of C/2 at 25° C. to obtain the discharge capacity. The discharge capacity was 126 mAh/g.
  • the cathode electrode layer containing the cathode active material, conductive agent and binder had high uniformity and thus the prepared positive electrode had high conductivity, capacity as well as stability.
  • a particulate cathode active material Li 1.01 Ni 0.53 Mn 0.30 Co 0.17 O 2 (NMC532) was obtained by a co-precipitation method followed by a calcination at 900° C.
  • the calcinated product was crushed by a ball milling for about 1.5 hours, followed by passing through a 270 mesh sieve to obtain a cathode active material having a particle size D50 of about 33 ⁇ m.
  • a positive electrode slurry was prepared by mixing 94 wt. % cathode active material prepared by method described above, 3 wt. % carbon black (SuperP; obtained from Timcal Ltd, Bodio, Switzerland) as a conductive agent, and 0.8 wt. % polyacrylic acid (PAA, #181285, obtained from Sigma-Aldrich, US), 1.5 wt. % styrene butadiene rubber (SBR, AL-2001, obtained from NIPPON A&L INC., Japan) and 0.7 wt. % polyvinylidene fluoride (PVDF; Solef® 5130, obtained from Solvay S.
  • PAA polyacrylic acid
  • SBR 1.5 wt. % styrene butadiene rubber
  • PVDF polyvinylidene fluoride
  • the homogenized slurry was coated onto one side of an aluminum foil having a thickness of 20 ⁇ m as a current collector using a doctor blade coater with a gap width of 100 ⁇ m.
  • the coated film on the aluminum foil was dried by an electrically heated conveyor oven at 65° C. at a conveyor speed of about 7 meters/minute.
  • the oven was arranged in a substantially windless environment. A wind speed between 0.3 m/s and 0.5 m/s inside the oven was detected.
  • the relative humidity inside the oven was 20-40%.
  • the drying time was about 3.5 minutes.
  • CR2032 coin-type Li cells were prepared by the method described in Example 3.
  • Electrochemical measurements of coin-type cells of Example 4 were performed by the method described in Example 3. The discharge capacity was 152 mAh/g.
  • the cathode electrode layer containing the cathode active material, conductive agent and binder had high uniformity and thus the prepared positive electrode had high conductivity, capacity as well as stability.
  • Cathode active material of Examples 5 and 6 were obtained from Xiamen Tungsten Co. Ltd, China.
  • the cathode slurries of Examples 5-7 were prepared by the method described in Example 1 except different parameters described in Table 1 below were used.
  • the coated cathode films of Examples 5-7 were dried by the method described in Example 1 except different drying conditions described in Table 2 below were used.
  • Example 2-7 The anode slurries of Examples 2-7 were prepared by the method described in Example 1.
  • the pouch cells of Examples 2-7 were assembled by the method described in Example 1.
  • the formulation of the cathode slurry of Examples 2-7 are shown in Table 1 below.
  • the drying conditions of the coated cathode film of Examples 2-7 are shown in Table 2 below.
  • the electrochemical performance of the pouch cells of Examples 2-7 are shown in Table 3 below.
  • a particulate cathode active material Li 1.02 Ni 0.33 Mn 0.35 Co 0.32 O 2 (NMC333) was obtained by a co-precipitation method followed by calcination at 850° C.
  • the calcinated product was crushed by a jet mill (LNJ-6A, obtained from Mianyang Liuneng Powder Equipment Co., Ltd., Sichuan, China) for about 2.5 hours, followed by passing through a 1,250-mesh sieve to obtain a cathode active material having a particle size D50 of about 6.5 ⁇ m.
  • a positive electrode slurry was prepared in the same manner as in Example 1, except that a cathode active material having a smaller particle size obtained by the method described in Comparative Example 1 was used.
  • the viscosity of the positive electrode slurry was 2,550 mPa ⁇ s.
  • a positive electrode comprising cathode active material obtained by the method described in Comparative Example 1 was prepared in the same manner as in Example 1, except that the coated film on the aluminum foil was dried at 85° C. and the drying time was about 10 minutes.
  • the positive electrode slurry of Example 1 dries more quickly than the positive electrode slurry of Comparative Example 1.
  • the particle size of the cathode active material influences the drying rate because as a particle becomes smaller, the surface area to volume ratio increases. The larger surface area allows a greater interaction with the solvent, resulting in slower drying. Therefore, cathode slurry of the present invention may lead to a more efficient drying process and improved productivity.
  • a particulate cathode active material LiMn 2 O 4 (LMO) was obtained by a solid-state reaction method followed by calcination at 900° C.
  • the calcinated product was crushed by a jet mill (LNJ-6A, obtained from Mianyang Liuneng Powder Equipment Co., Ltd., Sichuan, China) for about 2 hours, followed by passing through a 625-mesh sieve to obtain a cathode active material having a particle size D50 of about 7.5 ⁇ m.
  • a positive electrode slurry was prepared in the same manner as in Example 2, except that a cathode active material having a smaller particle size obtained by the method described in Comparative Example 2 was used.
  • the viscosity of the positive electrode slurry was 2,150 mPa ⁇ s.
  • a positive electrode comprising cathode active material obtained by the method described in Comparative Example 2 was prepared in the same manner as in Example 2, except that the coated film on the aluminum foil was dried at 75° C. and the drying time was about 9.5 minutes.
  • the positive electrode slurry of Example 2 dries more quickly than the positive electrode slurry of Comparative Example 2.
  • the particle size of the cathode active material influences the drying rate. Cathode slurry of the present invention may lead to a more efficient drying process and improved productivity.
  • Cathode active materials of Comparative Examples 5 and 6 were obtained from Hunan Rui Xiang New Material Co. Ltd, Changsha, China and HuaGuan HengYuan LiTech Co. Ltd., Qingdao, China respectively.
  • the cathode slurries of Comparative Examples 3-7 were prepared by the method described in Example 1 except different parameters described in Table 1 below were used.
  • the coated cathode films of Comparative Examples 3-7 were dried by the method described in Example 1 except different drying conditions described in Table 2 below were used.
  • the anode slurries of Comparative Examples 3-7 were prepared by the method described in Example 1.
  • Example 1 NMC333 42 46 2 2 NMP + Acetone 67.8 / 1,850 50
  • Example 2 LMO 15 46 1.5 2.5 Water + Ethanol 33.6 11.5 1,650 50
  • Example 3 LMO 28 47 1.5 1.5 Water 39 10.7 2,300 50
  • Example 4 NMC532 33 47 1.5 1.5 Acetone 135 / 2,550 50
  • Example 5 LFP 25 45 3 2 Water 32 10.2 2,960 50
  • Example 6 LCO 21 47 1.75 1.25 Water 39 10.3 2,750 50
  • Example 7 NMC532 30 46 2.25 1.75 Water 20 12.4 2,130 50
  • Comparative NMC333 6.5 46 2 2 NMP + Acetone 126 / 2,550 50
  • Example 1 Comparative LMO 7.5 46 1.5 2.5 Water + Ethanol 33.6 9.8 2,150 50
  • Example 2 Comparative LFP 25 45 3 2 NMP 0.79 / 3,020 50
  • Example 3 Comparative LCO 21 47 1.75 1.25 NMP 1 / 3,310 50
  • Example 4 Comparative NMC532 2 46 2.25 1.75 Water 20 1
  • Example 1 65 0.1-0.2 25-35 3
  • Example 2 60 0.3-0.5 25-40 4.5
  • Example 3 75 0.1-0.3 25-40 3
  • Example 4 65 0.3-0.5 20-40 3.5
  • Example 5 70 0.1-0.3 30-40 3.5
  • Example 6 75 0.3-0.5 30-45 4
  • Example 7 60 0.1-0.3 20-40 3 Comparative 85 0.1-0.2 25-35 10
  • Example 1 Comparative 75 0.3-0.5 25-40 9.5
  • Example 2 Comparative 70 0.1-0.3 30-40 13
  • Example 3 Comparative 75 0.3-0.5 30-45 12
  • Example 4 Comparative 60 0.1-0.3 20-40 6
  • Example 5 Comparative 75 0.1-0.3 25-40 3
  • Example 6 Comparative 100 0.1-0.2 25-40 3

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